Flexible magnetic plastic composition



United States Patent 3 379 643 FLEXIBLE MAGNETIC PLASTIC COMPOSITION Richard R. Merkel, Hackensack, NJ., assignor to Allied Chemical Corporation, New York, N.Y., a corporation of New York No Drawing. Filed Nov. 27, 1964, Ser. No. 414,433 6 Claims. (Cl. 252-6254) ABSTRACT OF THE DISCLOSURE The invention more specifically relates to new and improved highly flexible high magnetic strength compositions comprising a highly specific high molecular weight chlorinated polyethylene having chlorine content between 33-55% by weight, less than 3% residual polyethylene crystallinity and intrinsic viscosity between 3 to 6 in o-dichlorobenzene at 100 C., together with at least 30 parts of normally liquid plasticizer per 100 parts of the chlorinated polyethylene, and at least about 90% by total weight of fine magnetic particles having size less than about 10 microns.

The invention relates to plastic compositions and more particularly to synthetic plastic compositions having magnetic strength.

The combination of magnetic particles with a resinous binder enables the production of materials having both flexibility and magnetic strength. Such flexible magnets are of increasing interest for use in special applications such as door closure gaskets and, more particularly, because of their potential as a replacement for the more expensive and rigid metallic magnets used, for example, in electric motors. To improve efliciency and expand the application of the flexible magnets there is continued interest in providing plastic compositions containing more and more amounts of magnetic material and having correspondingly higher magnetic capacity. However, the provision of plastic magnets of high magnetic strength is not an easy matter as the product must have other properties which unfortunately are severely depreciated by the presence of increased amounts of magnetic material. Notably among such properties is flxeibility which can become so poor that cracking will be found on a single bending of a thin strip of the product. Thus, when attemp.ing to produce a strength flexible magnet containing about 90% magnetic material it has been found in the past that even thin strips of such compositions would crack on bending well before reaching an angle of 90. Further increase in magnet content have been found to produce compositions which are not capable of sustaining even a 45 bend without cracking. Such low flexibility not only reduces the attractiveness of the product but also renders manufacture and handling diflicult without high scrap loss due to cracking. Further, a major economic advantage of the plastic magnets rests basically in the ability to form or shape by molding or extrusion procedures, in contrast to the more expensive manufacturing operations required for the metallic magnets. Consequently, ability to process the high magnetic compositions by such conventional plastic forming techniques is also of major importance.

An object of the present invention is to provide new and improved filled plastic compositions combining high flexibility and high magnetic strength.

Another object is to provide new and improved flexible magnets of high magnetic strength suflicient for use in applications where metallic magnets have been employed.

Other objects and advantages will be evident from the following description of the invention.

In accordance with the invention it has been found 3,379,643 Patented Apr. 23, 1968 ICC that plastic composition of exceptionally high flexibility and magnetic strength is provided by combining fine magnetic particles with a highly specific chlorinated ethylene polymer which has been modified by addition of a normally liquid plasticizing material, the composition of the invention comprising: (A) 100 parts by weight of a chlorinated linear ethylene polymer having a chlorine content between about 33-55% by weight, less than 3% crystallinity as determined by differential thermal analysis, a glass transition temperature ranging from about minus 18 C. 1 10 C. for the 33% chlorine content chlorinated polyethylene up to about 63 C. i 15 C. for the 55% chlorine content chlorinated polyethylene, and high molecular weight corresponding to an intrinsic viscosity between 3 to 6 in o-dichlorobenzene at 100 C.; (B) at least 30 up to about 130 parts by weight, preferably 40-70 parts, of a normally liquid plasticizer for said chlorinated polyethylene; and (C) at least 1400 parts by weight of fine magnetic particles. The compositions provided by this invention contain at least about by weight of magnetic material and at such levels exhibit excellent flexibility as evidenced by bending through angles greater than 90". It has been also discovered that further increasing the magnetic particle content above about 92-93% by weight results in compositions in which .flexibility remains at a high level and is even improved over compositions containing less amounts of magnetic material. Hence, by the present invention it is possible to produce highly flexible magnetic compositions having magnetic particle content up to 95% by weight, or even more. In addition to high magnetic strength and flexibility the compositions of the present invention also combine good properties in general including good impact resistance, elongation, and tensile strength. The compositions may also be readily processed in conventional apparatus.

The compositions of the invention are based on a specific chlorinated polymer of ethylene having between about 33-55% by weight chemically combined chlorine and high molecular weight corresponding to an intrinsic viscosity of at least about 3 up to 6 in o-dichlorobenzene at C. The more preferred chlorinated polyethylenes have a chlorine content between about 35-50% and an intrinsic viscosity between about 3.5 to 5. The chlorinated polyethylenes employed in the invention are also characterized by having certain chlorine distribution on the basic polyethylene chain such that the chlorinated polymers have little or no crystallinity as determined by differential thermal analysis, the crystallinity of the polymers being less than about 3%, preferably 0% crystallinity. The chlorinated polyethylenes also have definitive glass transition temperatures varying with chlorine content of the polymers. The glass transition temperatures of the chlorinated polyethylenes employed in the invention range from about -18 C. 1*: 10 C. for the 33% chlorine content chlorinated polyethylene up to about 63 C. 15 C. for the chlorinated polymers having 55% by weight chlorine. The more preferred chlorinated polyethylenes have glass transition temperature ranging from about 15 C. i 10 C. for the 35% chlorine content chlorinated polyethylene up to about 35 C. :15 C. for the 50% chlorine con-tent chlorinated polyethylene. The chlorinated polymers employed in the present invention are also those prepared by chlorination of a linear, high density polyethylene. The terms linear" or substantially linear, as used herein in the appended claims, shall mean a polyethylene characterized by high density and at most only nominal short chain branching in the form of methyl groups, usually less than about 10 methyl groups per 1,000 carbon atoms in the molecule, more commonly 0 to 5 methyl groups per 1,000 carbon atoms.

The chlorinated polyethylenes by themselves will not accept the large amounts of magnetic particles required to form the compositions of the invention. In order to obtain compositions of high magnetic strength it is necessary to blend the chlorinated polyethylene with a plasticizing material which is a liquid under normal conditions. It has also been found that certain liquid plasticizers which are also surfactants, i.e. have surface active properties, will produce a substantial improvement in both magnetic strength and flexibility of the plastic magnets having a given amount of magnetic particles.

The amount of plasticizer required to be effective is at least about parts ranging up to about 120 parts per 100 parts of the chlorinated polyethylene. The more preferred compositions contain about to 70 parts of plasticizing material. The plasticizer employed in the composition is normally liquid material and plasticizers of this type are well known. Such plasticizers include, by way of example, the chlorinated aliphatic and aromatic hydrocarbons, the liquid epoxy resins such as those prepared by reaction of epichlorohydrin and bisphenol A, the epoxidized drying oils such as epoxidized soya bean oil and the monomeric and polyester plasticizers. The chlorinated hydrocarbons useful in the compositions of the invention have chlorine content generally between about 20% to 70% by weight and low molecular weight between about 200 to 4000. The more preferred chlorinated hydrocarbon plasticizers are the normally liquid chlorinated aliphatic hydrocarbons having chlorine content between about 30% to 55% and molecular weight between about 200 to 2000. The monomeric ester plasticizers are generally preferred and include those formed from the acid such as phosphoric, phthalic, adipic, sebacic, etc. Suitable alcohols for forming the monomeric esters have generally 2 to 16 carbon atoms, more usually 4 to 12 carbons. Examples of such monomeric plasticizers include tricresyl phosphate, diethyl phthalate, dibutyl phthalate, 2-ethylhexyl phthalate, dioctyl phthalate, butylcyclohexyl phthalate, didecyl phthalate, diisodecyl phthalate, diisobutyl phthalate, octyl decyl phthalate, diamyl phthalate, dicapryl phthalate, diethoxyethyl phthalate, dibutoxyethyl phthalate, dioctyl isophthalate, dioctyl adipate, and dibutyl sebacate. Generally, the more preferred plasticizers are the monomeric esters of phthalic acid. Certain liquid plasticizers are also known to have surface active properties and such materials have been found exceptionally beneficial in producing magnetic compositions combining both high magnetic strength and flexibility at a given loading at magnetic particles. Very suitable plasticizers of the surfactant type are the fatty acid esters of alcohols having 2 to 12 carbon atoms, preferably 3 to 8 carbon atoms. A specific example of such a fatty acid ester is butyl stearate. The surfactant plasticizers are employed in combination with the more conventional plasticizers and as little as about 2 parts per 100 parts of chlorinated polyethylene is effective in obtaining improved properties. The surfactant plasticizers may be employed in amounts representing between about 2-85% by weight of the total plasticizing materials with best results obtained when the surface active materials represent between about 30 75% of the total plasticizer. The surface active plasticizers are especially effective at the higher magnetic loading contents above about 92-93% where the association between the chlorinated polyethylene binder and magnetic particles becomes a critical factor obtaining both high flexibility and magnetic strength.

The chlorinated polyethylenes employed in practice of this invention are not readily or satisfactorily plasticized by conventional procedures at or about room temperatures. In preparation of the compositions this problem may be overcome by incorporation of the plasticizer for the chlorinated polyethylene at an elevated temperature about about 200 F. but not in excess of about 430 F. At such temperatures the chlorinated polyethylene will readily accept the plasticizing material and form therewith a composition of especially good homogeniety and also high flexibility and magnetic filler and loading content. The chlorinated polyethylene is subject to decomposition and thermal degradation at the higher temperatures and therefore it is desirable to first admix the chlorinated polyethylene with a heat stabilizer to protect the polymer against degration as it is subsequently heated to the plasticizing temperatures. The heat stabilizers employed may be those well-known materials commonly used with the chlorine-containing resins. Examples of such stabilizers include the inorganic salts and organic complexes of salts and metals such as barium, cadmium, tin, zinc, lead, sodium, etc. Also suitable are the liquid epoxy resins such as those prepared by reaction of epichlorohydrin and bisphenol A. The stabilizing materials also serve to protect the polymer during subsequent extrusion, molding or other forming operations conducted at elevated temperatures. The amount of heat stabilizer added is usually between about 1 to 15 parts to parts of the chlorinated polyethylene, more usually between about 2 to 10 parts. Admixing of the plasticizing material at elevated temperatures is satisfactorily accomplished in conventional compounding apparatus, for example, a Banbury mixer or rubber roll mill. Heating of the chlorinated polyethylene during mixing may be accomplished by supplying heat through the mixing apparatus and/ or the frictional heat of the mixing operation. The plasticizer may be initially admixed with the chlorinated polyethylene at room temperature or at elevated temperatures on the mixing apparatus either before or after the chlorinated polyethylene is heated to the desired elevated temperature. It is generally preferred in obtaining best results and efficient operation to rapidly heat the plasti-cizer and chlorinated polyethylene to the plasticizing temperature within a short period of about 5 minutes, preferably less than 3 minutes. This may be suitably accomplished by pre-heating of the mixing apparatus and/ or chlorinated polymer above about F. According to a preferred procedure the plasticizer is premixed with the chlorinated polyethylene and heat stabilizer in separate pre-mixing equipment and the resulting premix charged to the mixing apparatus, preferably a two roll rubber mill which has been preheated to a temperature near or above the plasticizing temperature, preferably between about 200 F. to 350 F. The plasticizing material is then readily combined with the chlorinated polyethylene above the plasticizing temperature and a homogeneous mass is found in a matter of minutes, usually between 1 to 10 minutes after charging to the mixing apparatus. The magnetic particles are then admixed with the resulting plasticized chlorinated polyethylene composition, preferably after adjusting the temperature of the mass to a reduced temperature between about l50-220 F. It has been found desirable when producing the highly filled magnetic compositions to add the magnetic particles in stages. For example, a preferred procedure involves the addition of a major portion but not all of the magnetic particles. After thorough mixing of the first charged particles the balance of the magnetic material may be added and mixing continued to form a homogeneous product. Such procedure aids in distribution of the magnetic particles in the binder and is also a factor in obtaining the combination high flexibility and magnetic strength. Another preferred method involves addition of the magnetic particles prior to heating of the polymer to the plasticization temperature to take advantage of the frictional heat generated by mixing of the solid filler material. The heatstabilized chlorinated polyethylene with or without the plasticizer is charged to a two roll mill which is preferably preheated to a temperature above about 150 F. usually between 180-230 F. After about 12 minutes mixing of the chlorinated polymer with the plasticizin-g material the magnetic particles are added, preferably in stages. Heat generated by mixing of the magnetic particles facilitates the rise in temperature of the mass such that the plasticizing temperature is reached within a short time and plasticization and formation of the filled composition readily obtained. In this procedure cooling of the mixing apparatus is recommended as by the use of ordinary water to control the temperatures below about 470 F. The composition sheeted out from the mill is especially suitable for extrusion, molding or other forming operations to produce a variety of flexible products. The magnetic material employed may be any of the well-known finely divided permanently magnetizable materials, it being also understood that the term magnetic may also mean magnetizable in view of the practical requirements of magnetizing the particles after combination with the binder. In the compositions the magnetic filler will have partcile size ranging from about 0.5 to 15 microns with average particle size preferably between about 1 to 3 microns. The more preferred magnetic fillers are those complex metal oxides well-known as ferrites which term, as used herein, designates an inorganic material of the formula MFe O wherein M is a divalent metal and m and n are whole numbers. The more preferred metal ferrites are the barium ferrites, for example, the barium ferrites represented by the formula BaFe O The chlorinated polyethylene is desirably prepared for use in the invention by chlorination of high molecular weight linear polyethylene in a heterogeneous medium in stages defined by introduction of chlorine at a temperature first below and then above the crystalline melting point of the polymer, as described in copending application of Pisanchyn et al., Ser. No. 86,309, filed Feb. 1, 1961, now abandoned. Preparation of the chlorinated olyethylene is most desirably accomplished by two-stage suspension chlorination of the linear, high molecular weight polyethylene with first-stage chlorination being carried out in aqueous slurry at temperature below the crystalline melting point of the ethylene polymer, preferably at a temperature of about 60 C. to 130 C., more usually at 90-120 C., until at least about 5 percent, preferably about percent, of chlorine has been introduced into the polymer. In the second stage the chlorination is continued in the aqueous slurry at a temperature above the crystalline melting point of the polymer but below the softening point of the chlorinated outer coating thereof until the desired chlorine is added. Second-stage chlorination temperatures are of the order of at least about 135 C. and preferably lie in the range of about 135 C. to 150 C. If desired. chlorination in the second-stage may be carried out at a temperature above the Crystalline melting point of the polymer for time sufficient to add at least about 5 percent chlorine by weight, preferably until at least a total of chlorine is added to the polymer, and the chlorination then continued at a lower temperature, e.g. 110 C. to 120 C., until the desired total chlorine is added.

The suitable chlorinated polyethylenes are derived from a linear polymer of ethylene having a molecular weight of at least about 700,000 ranging up to about 5,000,000, preferably between about 1,000,000 to 3,000,000. Chlorination of the linear polyethylene of 1-5 million molecular weight by the subject two-stage process will produce the particularly preferred chlorinated polyethylenes having 33-65 by weight chlorine and high molecular weight corresponding to an intrinsic viscosity within the range of at least about 3.5 in o-dichlorobenzene at 100 C. These preferred chlorinated polyethylenes are also chemically inert and insoluble at 2025 C. in organic solvents such as esters, acids and alcohols. They have tensile strength values according to ASTM Method D 63 8-5 8T (at drawing rate of 2 inches per minute) of at least about 2,500 p.s.i., usually between about 2,500 p.s.i. and about 4,500 p.s.i. The chlorinated polyethylenes also have true ultimate tensile strengths according to ASTM Method D 63858T of at least about 11,000 p.s.i., with the preferred materials of 3550% chlorin content having true ultimate tensile strength values between about 11,000 to 20,000. The chlorinated polyethylenes have less than about 3% crystallinity by differential thermal analysis, preferably 0% crystallinity, and also are characterized by low glass transition temperatures ranging from about minus 18 C.;L10

C. for the 33% chlorine material up to about 63 C.-* -15 C. for the 55% chlorine material. The preferred chlorinated polyethylenes have glass transition temperatures at least as low as about minus 15 C.:10 C. for the 35% chlorine material ranging to about 35 0:10 C. for the 50% chlorine content chlorinated polyethylene. The glass transition temperatures, a second order transition temperature, can be determined by plotting the stiffness modulus of the samples as a function of temperature, and can be defined as the temperature at which the stiffness modulus of the sample possesses a value of 1.45 10 p.s.i. or 10 dynes/cm. The determination may be made in accordance with ASTM Test D105361. In effect, the glass transition temperatureis that temperature below which the chlorinated polymers become brittle. Above the glass transition temperature the polymers become more flexible and rubbery. The low glass transition temperatures of the chlorinated polyethylenes contribute to the ability of the compositions of the invention to retain good elastomeric properties at low temperatures.

For preparation of the chlorinated polyethylene a particularly suitable linear high molecular weight polyethylene which may also be characterized by containing long chain polyethylene branches is produced, as described in British Patent 858,674 of June 11, 1961 to Allied Chemical Corporation, by gas phase polymerization of anhydrous, oxygen-free ethylene below the softening point of the polyethylene over a porous, frangible catalyst of an inorganic compound of chromium and oxygen and an active metal alkyl on a support of the group consisting of silica and silica-alumina. The polyethylenes produced thereby contain residue of the chromium-silica catalyst systems dispersed throughout the polyethylene is an amount of at least about 001%, usually .001.002%, by weight. The chromium-silica catalyst material added during polymerization is retained in the polyethylene during chlorination and contributes to the properties of the chlorinated polyethylene. Prior to chlorination the polyethylene from which the chlorinated polyethylene is derived has a density between about 0.935 and about 0.985 and a crystallinity of at least and customarily in the range of 75% to as determined, for example, by differential thermal analysis. The preferred polyethylenes produced by British Patent 858,674 have weight average molecular weight between 1.0 million and about 5.0 million, preferably between 1.0 to 3.5 million, as calculated according to the method of P. S. Francis et al. from the viscosity of about 0.05 to 0.1 gram per 100 cc. solution in decalin at 135 C. using the equation:

n=intrinsic viscosity M =weight average molecular weight (I. Polymer Science,

vol. 31, pp. 453466, September 1958) The following examples in which parts and percentages are by weight demonstrate the practice and advantages of the present invention.

Examples 1-6 Chlorinated polyethylene of 45% chlorine was prepared by staged aqueous chlorination of linear polyethylene having a weight average molecular weight of about 1.5 million and density of 0.94. The polyethylene employed was prepared in accordance with British Patent 858,674 (Example 6) by gas phase polymerization of anhydrous oxygen-free ethylene over a catalyst of magnesium dichrornate on a porous support with aluminum triisobutyl. The support was composed of silica and 10% aluminum. Chlorination of the polyethylene in a first stage was carried out at a temperature of about C. until 17% chlorine was added to the ethylene polymer followed by second stage chlorination at a temperature of 140 C. until a total of about 35 chlorine was added. Chlorination was then continued at a temperature of about 110-l20 C. until a total of 45% by weight chlorine was added. The chlorinated polyethylene recovered from the slurry was washed and dried overnight at a temperature of 60 C. The chlorinated polyethylene had a glass transition temperature of about 5 C. (ASTM D105363) and crystallinity as measured by differential thermal analysis. The chlorinated polyethylene also had high molecular weight corresponding to an intrinsic viscosity of 4.0 in o-dichlorobenzene at 100 C.

A series of magnetic compositions was prepared by the following procedure from the above prepared chlorinated polyethylene. 100 parts of the chlorinated polymer was admixed with 3 parts of a barium-cadmium organic heat stabilizer obtained from the National Lead Company under the trademark Temex C. There was also added about 58 parts of dioctyl phthalate as plasticizer and about 0.5 part of stearic acid as lubricant. Each of the compositions contained barium ferrite as magnetic filler in varying amounts between about 1400 to 2400 parts by weight. The barium ferrite had an average particle size of about 1-2 microns. In preparing each of the compositions between about 90-95% of the total barium ferrite was added and the resulting components charged to a two roll (6 inch x 12 inch) differential speed rubber mill which had been preheated to a temperature of about 300 F. by internal steam heating of the two mill rolls. After about two minutes on the mill the temperature of the mixture was increased to about 300 F. and fluxed. Mixing of the charge was then continued for an additional 510 minutes during which a homogeneous mass was formed. The temperature of the mixture was then reduced to about 180 F. over the course of about minutes and there was then added to the mixture the remaining 510% of barium ferrite. Mixing on the mill was then continued for an additional 3-5 minutes to form a homogeneous mass which was sheeted out from the mill to form sheets of 0.14 inch thickness. Specimens of each of the compositions were then evaluated and the results are tabulated below in Table I.

TABLE I Example No 1 2 3 4 5 6 Barium Ferrite, Parts by weigh 1,449 1.628 1,740 1,890 2,000 2,316 Bcrium Ferrite, percent by Crack Angle 90 80 00 51 50 Mandrel Bend, 1 inch mandrel 180 180 180 180 60 50 Magnetic Strength at 0.015

inch gap 2 0.221 0.238 0.250 0.229

1 Determined with 2 inch specimen on Tinius Olsen Stitiness Testcr at. 50 load dial reading employing a 0905 pound calibrating weight. Maximum angle obtainable in stiffness tester is 90.

2 Lbs. lift pre inch length.

Examples 7-10 A series of four additional compositions were prepared employing components and procedure similar to Example 1 except that the plasticizing material was a combination of 23 parts dioctyl phthalate and parts butyl stearate. These compositions were then evaluated as in Examples 1-6 and the results are in Table II.

tabulated below at 50 load dial reading employing a 0.093 pound calibrating weight. Maximum angle obtainable in stillness tester 13 2 Lbs. lilt per inch length.

The Table II compositions all have excellent flexibility and high magnetic strength which increases approx mateiy proportionately with the amount of magnetic particles. Table II also clearly demonstrates the ability of the compositions of the invention to exhibit improved flexibility along with high magnetic strength upon increase of the amount of magnetic particles above about 92%. Hence, the composition of Example 9 containing 92% magnetic particles has a crack angle of 50 and mandrel bend of about 135 while the composition of Example 10 containing some 300 parts more of the particles has substantially improved flexibility with a crack angle greater than 90 and flexibility around the 1 inch mandrel of 180. The Table II also clearly demonstrates the eiiectiveness of the butyl stearate in improving magnetic strength, particularly at the higher contents of magnetic particles. Hence, the composition of Example 10 containing 93% magnetic material has superior magnetic strength and also flexibility over the composition of Example 6 containing 93.5% magnetic particles.

Although certain preferred embodiments of the invention have been disclosed for purpose of illustration, it will be evident that various changes and modifications may be made therein without departing from the scope and spirit of the invention.

I claim:

1. A highly flexible highly magnetic plastic composition comprising a binder of a chlorinated linear polymer of ethylene and at least 30 parts up to about 130 parts of a normally liquid plasticizer per parts of the chlorinated polyethylene and at least about 90% by weight of fine magnetic particles having size less than about 10 microns, said chlorinated polyethylene having a chemically combined chlorine content between 33-55% by weight, less than 3% crystallinity as determined by differential thermal analysis, glass transition temperature ranging from about minus 18 C.il0 C. for the 33% chlorine content chlorinated polyethylene up to about 63 C.i-15 C. for the 55% chlorine content chlorinated polyethylene, and molecular weight corresponding to an intrinsic viscosity between about 3 to 6 in o-dichlorobenzene at 100 C.

2. The composition of claim 1 in which the chlorinated polyethylene has a chlorine content between about 3550% by weight and 0% crystallinity as measured by diiferential thermal analysis.

3. Thecomposition of claim 1 in which the amount of plasticizer is between about 40-70 parts.

4. A highly flexible highly magnetic plastic composition comprising a binder of a chlorinated linear polymer of ethylene and between about 30 to parts per 100 parts of the chlorinated polyethylene of a normally liquid plasticizer of which between 2-85% by weight is a plasticizer which is also a surfactant and at least about 90% by weight of fine magnetic particles having size less than about 10 microns, said chlorinated polyethylene having a chemically combined chlorine content between 3550% by weight, 0% crystallinity as determined by differential thermal analysis, glass transition temperature ranging from about minus 15 -C.i-10 C. for 35% chlorine content chlorinated polyethylene up to about 9 10 35 C.-* -l5 C. for the 50% chlorine content ehlo- References Cited rinated polyethylene, and molecular weight corresponding FOREIGN PATENTS to an intrinsic viscosity between about 3 to 6 o-dichlorobenzene at 100 C. 1,323,095 2/1963 France.

5. The composition of claim 4 in which the amount of liquid plasticizer is between about 40-70 parts of which between about 3075% by weight is a fatty acid ester of an alcohol of 2-12 carbon atoms. 53 PVC technology 1962 7346 98 and 6. The composition of claim 4 in which the liquid piasticizer is a mixture of a phthalate plasticizer and be- TOB L O E tween about 30-75% parts by total plasticizer weight of 10 IAS R EV P'lmary xamme" butyl stem-ate ROBERT D. EDMONDS. Examiner.

OTHER REFERENCES Kres-ser: Polyethylene, 1957, p. 64. 

